CN102432864A - Method for reducing content of quinine in polyphenyl ether product and recovering biphenyl diquinone - Google Patents
Method for reducing content of quinine in polyphenyl ether product and recovering biphenyl diquinone Download PDFInfo
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- CN102432864A CN102432864A CN2011102556028A CN201110255602A CN102432864A CN 102432864 A CN102432864 A CN 102432864A CN 2011102556028 A CN2011102556028 A CN 2011102556028A CN 201110255602 A CN201110255602 A CN 201110255602A CN 102432864 A CN102432864 A CN 102432864A
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Abstract
The invention relates to a method for reducing the content of quinine in a polyphenyl ether product and recovering biphenyl diquinone, comprising the following steps of: (1) rising the temperature of reaction products from preparation of polyphenyl ether by a precipitation method to be 55-65 DEG C, balancing and obtaining polyphenyl ether mixed liquid; (2) filtering the polyphenyl ether mixed liquid, washing for four times, drying filter cakes and obtaining the polyphenyl ether; (3) taking the filtrate in the previous two times, filtering, washing the filter cakes with acetone and pure water in sequence, drying and obtaining a biphenyl diquinone crude product; and (4) carrying out precipitation, filtering and drying on the biphenyl diquinone crude product and obtaining the biphenyl diquinone. In the method, the operation process is simple, the purity of the recovered biphenyl diquinone is high, the content of the quinine in the polyphenyl ether product can also be reduced, and the industrial application prospect is larger.
Description
Technical field
The present invention relates to chemical field, be specifically related to a kind of method that reduces quinone content in the ppe product and reclaim the biphenyl diquinone.
Background technology
Usually the production of ppe has two kinds of methods: precipitation method and solution method, and no matter which kind of working method is at oxidative coupling 2, and by product biphenyl diquinone (3 invariably accompanies in the process of 6-xylenol generation ppe; 3; 5,5-tetramethyl--4,4-biphenyl diquinone) generation.It is a kind of behind reaction terminating that U.S. Pat 4234706 provides; Make biphenyl diquinone and ppe generation redistribution reaction reduce the method for quinone content in the ppe under the high temperature; Relatively be suitable for solution method; But be not suitable for precipitation method, for precipitation method,, carry out redistribution reaction with the biphenyl diquinone even be difficult under the high temperature because ppe is separated out as particle yet.Providing a kind of in the U.S. Pat 4060514 contacts with ppe in the presence of consisting of phase-transferring agent with dithionate or thiosulfuric acid reductive agent; Remove the method for biphenyl diquinone; Though it is this method is applicable to precipitation method production, not ideal enough with the ppe color that this method obtains.Provide a kind of mixture to make the biphenyl diquinone become the method for halogenated biphenyl quinone among the U.S. Pat 3637593A with hydrogen halide processing ppe and biphenyl diquinone; Remaining in the ppe halogen element arranged but this kind method may make, cause the antioxygen bad stability of ppe.Provide among the Chinese patent CN101717501A that a kind of to proceed to ppe monomer polymerization degree at monomer phenols oxidative coupling be that 50-95% carries out solid-liquid separation earlier and continues polyreaction again and reach the polymerization method that reduces biphenyl diquinone in the polyphenylene oxide resin; Though this method can effectively reduce the content of biphenyl diquinone in the polyphenylene oxide resin, prepares the process relative complex.
As by product biphenyl diquinone; Higher utility is arranged; It is a kind of important active intermediate, can synthesize the fire retardant material of good heat resistance, good mechanical performance, also can be used as the initiator of ppe redistribution reaction; Be used for synthetic multiple hydroxyl aryl oxide, distant pawl, block, grafting, comb type and star-type polymer, the good resin laminated material of polyphenylene oxide/epoxy that is used for high frequency printed circuit board of processability.In addition, also can be used as coupling agent uses.At present, the biphenyl diquinone can emit with oligopolymer usually in the process of precipitation method production ppe, is not efficiently recovered and utilizes, and has caused certain waste.
Summary of the invention
In order to overcome above-mentioned defective, the purpose of this invention is to provide quinone content in a kind of simple and effective reduction ppe product and reclaim the method for quinone.
The method of quinone content and recovery biphenyl diquinone comprises the steps: in the reduction ppe product of the present invention
(1) reaction product that precipitation method is prepared ppe is warming up to 55～65 ℃, balance, the ppe mixed solution;
(2) filter the ppe mixed solution, wash four times, dry cake gets ppe;
(3) get preceding twice filtrating, filter, successively with acetone, pure water washing leaching cake, drying obtains biphenyl diquinone bullion;
(4) biphenyl diquinone bullion is carried out precipitating, filtration and drying, obtain the biphenyl diquinone.
Wherein, Precipitation method described in the step (1) prepares ppe: under the condition that feeds nitrogen; In the reaction solution that ppe good solvent, poor solvent, metal salt solution, amine compound constitute, feed oxygen-containing gas oxidative coupling 2; The 6-xylenol is to contain the aqueous solution termination reaction of complexing agent;
Wherein, said good solvent is one or more in chloroform, toluene, benzene or the YLENE; Said poor solvent is one or more in methyl alcohol, ethanol, Virahol, propyl carbinol or the butanone.
In addition, the said balance time of step (1) is 0.5～1.5h.
In addition, the described washing of step (2) is followed successively by for four times:
With toluene by weight per-cent is that 20～40% methylbenzene methanol mixed solution carries out the washing first time;
With toluene by weight per-cent is that 10～20% methylbenzene methanol mixed solution carries out the washing second time;
With toluene by weight per-cent is that 5～10% methylbenzene methanol mixed solution washs for the third time;
With weight percent is that 100% methanol solvate carries out the 4th washing.
In addition, when the washing described in the step (2) four times, temperature is 45～55 ℃.
In addition, in step (3), the consumption of acetone is that the consumption of more than 3 times of filter cake weight, pure water is more than 4 times of filter cake weight.
In addition, the temperature of said pure water is more than 60 ℃.
In addition, precipitating is described in the step (4): while stirring biphenyl diquinone bullion is added in the toluene, be warming up to 50～100 ℃, constant temperature stirs, and adds methyl alcohol, is cooled to the biphenyl diquinone and separates out.
Wherein, the weight ratio of said biphenyl diquinone bullion and toluene was greater than 1: 10, and the weight ratio of toluene and methyl alcohol is 1: 0.6～1: 4.0.
In addition, the time that said constant temperature stirs is more than the 0.5h, and the speed of said cooling is less than 3 ℃/min.
Wherein, Good solvent can be to account for total solution weight below 60% in the said precipitation method; Ppe is separated out; Said metal-salt can be the mixture of Red copper oxide and hydrogen bromide solution; Said amine compound is be selected from diamine compound, monobasic tertiary amine and monobasic secondary amine compound at least a, and said complexing agent can be elected as and be selected from least a of Hydrocerol A, disodium edta, ethylene diamine tetramethylene phosphonic acid, HEDP, hydroxyethylethylene diamine tri-acetic acid, diethylene triamine pentacetic acid (DTPA), but the present invention is not limited thereto.
The reaction product that among the present invention precipitation method is prepared ppe is warming up to 55～65 ℃; And keep for some time, purpose is to guarantee can fully dissolve at the by product biphenyl diquinone crystal that the low-temp reaction stage generates and separates out, again through filtering and washing; Reach the purpose that reduces biphenyl two quinone contents in the ppe product; Wherein, wash temperature is not less than 45 ℃, can prevent that with the washing of the mixed solution of toluene and methyl alcohol the quinone in the filter cake from separating out again.
The present invention is to filtering ppe mixed solution washing four times, and purpose is to obtain the high ppe of purity, and the biphenyl diquinone that is wherein generated is included in the first time, the secondary filtrating above 99% amount, only need collect preceding twice filtrating when reclaiming the biphenyl diquinone and get final product.The biphenyl diquinone separates out and deposits to container bottom under the low temperature with crystalline form, and a small amount of filtrating that the major part filtrating on removable top only keeps the bottom before therefore filtering alleviates and filters load.
Biphenyl two quinone contents are measured with spectrophotometer method in the ppe, and unit is PPM.
The purity of biphenyl diquinone is tested with melting point detector, and unit is ℃.
Biphenyl two quinone contents are low in the ppe that obtains through the present invention, and below 10ppM, the biphenyl diquinone chemical name of recovery is 3 mostly; 3,5,5-tetramethyl--4; 4-biphenyl diquinone, crystal color is scarlet, crystal grain is thin and purity is higher, and fusing point is 202 ℃～203 ℃.Method technology provided by the present invention is simple, and is easy to implement and production efficiency is high.
Embodiment
Following examples are used to explain the present invention, but are not used for limiting scope of the present invention.
Embodiment 1
Under the condition that feeds nitrogen; In the reaction solution that constitutes by ppe good solvent toluene 225g, poor solvent methyl alcohol 225g, metal salt solution 3g, amine compound 9.45g, feed oxygen-containing gas oxidative coupling 150g2; The 6-xylenol is to contain 1.3g complexing agent lemon aqueous acid termination reaction;
Stop behind the logical oxygen product being warming up to 55 ℃; Continue to stir balance 1.0h; Filter and carry out the first time with the methylbenzene methanol mixing solutions 200g of toluene by weight per-cent 35% and wash; Carry out the washing second time with the methylbenzene methanol mixing solutions 600g of toluene by weight per-cent 15%, with toluene by weight per-cent 7.5% mixing solutions 600g wash for the third time, carry out the 4th time with methanol solvate 300g at last and wash; 45 ℃ of wash temperatures are afterwards with the dry ppe powder 142.5g that gets of high temperature nitrogen.Collect for the first time filtrating and filtrate in container for the second time, leave standstill after being cooled to below 20 ℃, leave standstill 0.5h, remove the most solutions on top, filter the back and be higher than 60 ℃ hot wash, getting biphenyl diquinone bullion 3.95g behind the filtration cakes torrefaction with 25g acetone and 40g.
40g good solvent toluene is added in the container of band stirring; Add biphenyl diquinone bullion while stirring, be warming up to 60 ℃, after continuing to stir 0.5h; Add 24g methyl alcohol and be cooled to 20 ℃ and under this temperature, leave standstill 0.5h, filter, dry biphenyl diquinone with the speed of 3 ℃/min.Experimental result is listed in the table 1.
Embodiment 2
According to carrying out the recovery of polymerization and biphenyl diquinone with embodiment 1 identical mode, just stop polyreaction after, reactant is warming up to 55 ℃, balance 1.5h.Experimental result is listed in the table 1.
Embodiment 3
According to carrying out the recovery of polymerization and biphenyl diquinone with embodiment 1 identical mode, just stop polyreaction after, reactant is warming up to 60 ℃, balance 1.5h.Experimental result is listed in the table 1.
Embodiment 4
According to carrying out the recovery of polymerization and biphenyl diquinone with embodiment 1 identical mode, just in the precipitating, the poor solvent methanol usage is 160g.Experimental result is listed in the table 1.
Embodiment 5
According to carrying out the recovery of polymerization and biphenyl diquinone with embodiment 1 identical mode; When just filtering the polymerisate behind the constant temperature; Methylbenzene methanol mixing solutions with 200g toluene by weight per-cent 20% carries out the washing first time; Carry out the washing second time with the methylbenzene methanol mixing solutions of 600g toluene by weight per-cent 15%, wash for the third time, carry out the 4th washing with the 300g methanol solution with the methylbenzene methanol mixing solutions of 600g toluene by weight per-cent 10%; And during biphenyl diquinone bullion precipitating, the speed with 2 ℃/min behind the adding methyl alcohol is cooled to 20 ℃.Experimental result is listed in the table 1.
The comparative example 1
According to carrying out the recovery of polymerization and biphenyl diquinone with embodiment 1 identical mode, just stop polyreaction after, be warming up to 50 ℃, balance 1.0h.Experimental result is listed in the table 1.
The comparative example 2
According to carrying out the recovery of polymerization and biphenyl diquinone with embodiment 1 identical mode, three washings change into methanol solvate and washing when just washing the ppe mixed solution, and usage quantity is constant.
The comparative example 3
According to carrying out the recovery of polymerization and biphenyl diquinone with embodiment 1 identical mode, secondary washing changes into methanol solvate and washing when just washing the ppe mixed solution, and usage quantity is constant.
Experimental result is listed in the table 1.
The comparative example 4
According to carrying out the recovery of polymerization and biphenyl diquinone with embodiment 1 identical mode, once washing changes into methanol solvate and washing when just washing the ppe mixed solution, and usage quantity is constant.
Experimental result is listed in the table 1.
The comparative example 5
According to carrying out the recovery of polymerization and biphenyl diquinone with embodiment 1 identical mode, just in the precipitating, the poor solvent methanol usage is 20g.Experimental result is listed in the table 1.
The comparative example 6
According to carrying out the recovery of polymerization and biphenyl diquinone with embodiment 1 identical mode, the poor solvent methanol usage is 200g.Experimental result is listed in the table 1.
The comparative example 7
According to carrying out the recovery of polymerization and biphenyl diquinone with embodiment 1 identical mode, just cooling rate is 5 ℃/min.Experimental result is listed in the table 1.
Table 1
From table 1, can find out; From comparative example 2～4, can find out; The influence of quinone content is still comparatively tangible in the different polyphenylene ether of mode of washing; Can find out that from comparative example 4～7 data the amount of methyl alcohol the precipitating crosses the low output that can reduce the biphenyl diquinone, the too much or too fast meeting of cooling rate of methyl alcohol add-on makes the foreign matter content increase in the biphenyl diquinone product that the fusing point of biphenyl diquinone is reduced.
Through according to method provided by the invention; Can effectively reduce precipitation method particularly and produce the content of the biphenyl diquinone in the ppe product; But also can when improving the ppe product quality, obtain the higher biphenyl diquinone of purity; Compare the production efficiency with improvement with previous methods also more effective, can fully satisfy the requirement of industrial community.
With describing in detail and invention has been described with reference to concrete embodiment, but those skilled in the art should be understood that under the situation that does not deviate from spirit of the present invention and protection domain and can carry out various changes and modifications.
Claims (10)
1. a method that reduces quinone content in the ppe product and reclaim the biphenyl diquinone is characterized in that, comprises the steps:
(1) reaction product that precipitation method is prepared ppe is warming up to 55～65 ℃, balance, the ppe mixed solution;
(2) filter the ppe mixed solution, wash four times, dry cake gets ppe;
(3) get preceding twice filtrating, filter, successively with acetone, pure water washing leaching cake, drying obtains biphenyl diquinone bullion;
(4) biphenyl diquinone bullion is carried out precipitating, filtration and drying, obtain the biphenyl diquinone.
2. method according to claim 1; It is characterized in that; Precipitation method described in the step (1) prepares ppe: under the condition that feeds nitrogen; In the reaction solution that ppe good solvent, poor solvent, metal salt solution, amine compound constitute, feed oxygen-containing gas oxidative coupling 2, the 6-xylenol is to contain the aqueous solution termination reaction of complexing agent;
Wherein, said good solvent is one or more in chloroform, toluene, benzene or the YLENE; Said poor solvent is one or more in methyl alcohol, ethanol, Virahol, propyl carbinol or the butanone.
3. method according to claim 1 is characterized in that, the said balance time of step (1) is 0.5～1.5h.
4. method according to claim 1 is characterized in that, the described washing of step (2) is followed successively by for four times:
With toluene by weight per-cent is that 20～40% methylbenzene methanol mixed solution carries out the washing first time;
With toluene by weight per-cent is that 10～20% methylbenzene methanol mixed solution carries out the washing second time;
With toluene by weight per-cent is that 5～10% methylbenzene methanol mixed solution washs for the third time;
With weight percent is that 100% methanol solvate carries out the 4th washing.
5. method according to claim 1 is characterized in that, when the washing described in the step (2) four times, temperature is 45～55 ℃.
6. method according to claim 1 is characterized in that, in step (3), the consumption of acetone is that the consumption of more than 3 times of filter cake weight, pure water is more than 4 times of filter cake weight.
7. method according to claim 6 is characterized in that, the temperature of said pure water is more than 60 ℃.
8. method according to claim 1 is characterized in that, precipitating is described in the step (4): while stirring biphenyl diquinone bullion is added in the toluene, be warming up to 50～100 ℃, constant temperature stirs, and adds methyl alcohol, is cooled to the biphenyl diquinone and separates out.
9. method according to claim 8 is characterized in that, the weight ratio of said biphenyl diquinone bullion and toluene was greater than 1: 10, and the weight ratio of toluene and methyl alcohol is 1: 0.6～1: 4.0.
10. method according to claim 8 is characterized in that, the time that said constant temperature stirs is more than the 0.5h, and the speed of said cooling is less than 3 ℃/min.
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| CN 201110255602 CN102432864B (en) | 2011-08-31 | 2011-08-31 | Method for reducing content of quinine in polyphenyl ether product and recovering biphenyl diquinone |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107236124A (en) * | 2016-03-28 | 2017-10-10 | 旭化成株式会社 | The manufacture method of polyphenylene oxide |
| CN110078912A (en) * | 2018-01-26 | 2019-08-02 | 蓝星（北京）技术中心有限公司 | A kind of polyphenylene oxide continuous pressure filtration washing methods |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4237265A (en) * | 1975-09-08 | 1980-12-02 | General Electric Company | Process for catalyst removal from polyphenylene ether reaction solutions |
| CN101423604A (en) * | 2008-11-21 | 2009-05-06 | 中国蓝星（集团）股份有限公司 | Method for filtering polyphenylene oxide precipitate in polyphenylene oxide solvent recovery system |
| CN101717501A (en) * | 2009-11-30 | 2010-06-02 | 中国蓝星（集团）股份有限公司 | Polymerization method for reducing content of reaction byproduct in polyphenylene oxide resin |
-
2011
- 2011-08-31 CN CN 201110255602 patent/CN102432864B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4237265A (en) * | 1975-09-08 | 1980-12-02 | General Electric Company | Process for catalyst removal from polyphenylene ether reaction solutions |
| CN101423604A (en) * | 2008-11-21 | 2009-05-06 | 中国蓝星（集团）股份有限公司 | Method for filtering polyphenylene oxide precipitate in polyphenylene oxide solvent recovery system |
| CN101717501A (en) * | 2009-11-30 | 2010-06-02 | 中国蓝星（集团）股份有限公司 | Polymerization method for reducing content of reaction byproduct in polyphenylene oxide resin |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107236124A (en) * | 2016-03-28 | 2017-10-10 | 旭化成株式会社 | The manufacture method of polyphenylene oxide |
| CN110078912A (en) * | 2018-01-26 | 2019-08-02 | 蓝星（北京）技术中心有限公司 | A kind of polyphenylene oxide continuous pressure filtration washing methods |
| CN110078912B (en) * | 2018-01-26 | 2021-11-09 | 蓝星（北京）技术中心有限公司 | Continuous pressure filtration washing method for polyphenyl ether |
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Effective date of registration: 20180705 Address after: 226017 JIANGGANG Road, Nantong economic and Technological Development Zone, Jiangsu 118 Patentee after: Xingchen Synthetic Matrials Co., Ltd., Nantong Address before: 100083 6518 Garden Hotel, Garden East Road, Haidian District, Beijing, 6518 Patentee before: Lanxing Chemical New Material Co., Ltd. |
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